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Low viscosity oligomer oil product, process and composition

a technology of oligomer oil and low viscosity, applied in the field of low viscosity oligomer oil product, process and composition, can solve the problems of limited supply of 1-decene and add complexity, and achieve the effects of low noack volatility, low pour point and high viscosity index

Active Publication Date: 2013-08-29
INEOS USA LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The present invention addresses a shortage of traditional 4 cSt PAO used in high performance oils and proposes the use of alphaolefins feedstock to generate a complementary 4 cSt PAO with critical properties similar or better than existing commercial products. The invention provides that the new PAO is interchangeable with existing commercial products under the ATIEL Read Across procedure and has similar or better properties than existing commercial products in terms of VI and Noack performance, cold crank viscosity, tertiary hydrogens, thermal stability, flash point, additive solubility, traction coefficient, and additives response. The invention has been developed on laboratory and semi-industrial facilities and results from lab scale to industrial scale equipment show equivalently or superior performance of the present invention compared to existing commercial products.

Problems solved by technology

However, 1-decene is in limited supply because it is a co-product made together with a broad range of other alpha olefins.
Additionally, a problem associated with making oligomer oils from 1-decene or other alpha olefins is that the oligomer product mix usually must be fractionated into different portions to obtain oils of a given viscosity (e.g. 2, 4, 6, or 8 cSt at 100° C.).
This adds complexity by requiring an initial dimerization of the vinylidene to at least about 50 weight percent dimer.

Method used

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  • Low viscosity oligomer oil product, process and composition
  • Low viscosity oligomer oil product, process and composition
  • Low viscosity oligomer oil product, process and composition

Examples

Experimental program
Comparison scheme
Effect test

example 1

[0089]A 1-gallon Parr reactor equipped with jacketed heating and internal cooling was charged with 515.0 g 1-tetradecene and 885.0 of C16 vinylidene (89% vinylidene olefin, 8% internal olefin, and 3% trisubstituted olefin by H NMR), 1.4 g 1-butanol, and 1.4 g butyl acetate and was taken to 30° C. with stirring. Boron trifluoride was introduced and it was adjusted to a steady state pressure of 20 psi; an immediate exotherm to 43° C. was observed which was controlled within 3 minutes. The reaction was stirred for 30 minutes. The oligomerization reaction was also conducted in manner that portion or all of the reactants are added slowly to the Parr reactor for a better control of the exotherm; it can also be performed in a continuous mode employing 2-5 continuous stirred tank reactors (CST) in series or parallel. The reaction mixture quenched with 400 ml 8% NaOH and washed with distilled water. Removal of unreacted and volatile fluids under reduced pressure (200° C., 0.1 mmHg) resulted ...

examples 2-4

[0126]Mole ratios of C16 / C14 examples provide that the Mole ratios were optimized to obtain PAOs with enhanced viscometric properties; high C14 character in the product adversely impacts Pour Point (high Pour Point). Table below shows examples highlighting impact of C16vd / C14 mole ratios on Pour Point properties of resultant fluids under similar conditions:

TABLE 2C16vd / C14 MolePourExamplesRatioPoint° C.11.5−6321.2−4531.0−4240.8−39

examples 5

[0127]The 1 gallon oligomerization Parr reactor was charged under an inert N2 atmosphere with 515.0 g 1-tetradecene (INEOS C14), 885.0 g C16 vinylidene (89% vinylidene olefin, 8% internal olefin, and 3% trisubstituted olefin by H NMR), 2.8 g butyl acetate and was taken to 30° C. with stirring. Boron trifluoride was introduced and it was adjusted to a steady state pressure of 20 psi; an immediate exotherm to 38° C. was observed which was controlled within 3 minutes by the action of chiller and brought back to 30° C. The reaction was stirred at this temperature for 30 minutes, excess BF3 was expelled through the caustic scrubber and the reaction medium was further purged for 15 minutes with N2. The crude reaction mixture was quenched with 400 ml 8% NaOH and the separated organic phased was further washed with distilled water. Removal of unreacted and volatile fluids under reduced pressure (200° C., 0.1 mmHg) resulted in isolation of 1092.2 g of a clear fluid which was hydrogenated und...

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Abstract

The present invention relates to a low viscosity lubricant process, product, and composition characterized by low Noack volatility, low pour point, useful low temperature viscometrics, and high viscosity index and more particularly concerns a PAO composition having a kinetic viscosity at 100° C. in the range of about 4 cSt.

Description

[0001]This application is a divisional application of U.S. application Ser. No. 12 / 734,830, filed Oct. 25, 2010, which is a nationalization under 35 U.S.C. 371 of International Patent Application No. PCT / US2008 / 013157, filed Nov. 26, 2008, which claims benefit of priority to U.S. Provisional Application No. 61 / 004,741, filed Nov. 29, 2007 and U.S. Provisional Application No. 61 / 008,378, filed Dec. 20, 2007.FIELD OF THE INVENTION[0002]Oligomers of alpha olefins (also known as linear alpha olefins or vinyl olefins), and their use in the formulation of synthetic and semi-synthetic lubricants is known in the art.[0003]Traditionally, the alpha olefin oligomers that have proved useful as synthetic base fluids are prepared mainly from linear terminal olefins containing about 8-14 carbon atoms such as 1-octene, 1-decene, 1-dodecene, 1-tetradecene and mixtures thereof. One of the most widely used alpha olefins is 1-decene which can be used alone or in a mixture with other alpha olefins. When...

Claims

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Application Information

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IPC IPC(8): C07C11/02C07C2/20C10M105/04
CPCC07C11/02C10G2400/10C07C2/20C10G50/02C10M105/04C10G2300/1092C10G2300/1088C10G45/00C10N2270/00C10N2260/02C10M107/10C10M2205/006C10M2205/0285C10M2207/026C10M2207/2835C10M2215/06C10M2215/223C10M2223/04C10N2220/021C10N2220/022C10N2220/023C10N2220/025C10N2220/028C10N2230/02C10N2230/10C10N2230/74C10N2240/04C10N2240/10C10N2240/102C10N2240/30C10M2203/1006C10M2203/1025C10M2205/022C10M2205/024C10M2205/06C10M2205/22C10M2207/028C10M2209/084C10M2215/28C10M2219/02C10M2219/024C10M2219/046C10M2223/045C10N2240/12C10M2205/028C10N2020/04C10N2020/02C10N2020/011C10N2020/065C10N2020/071C10N2030/02C10N2030/10C10N2030/74C10N2040/04C10N2040/25C10N2040/252C10N2040/12C10N2040/30C10N2060/02C10N2070/00
Inventor BAGHERI, VAHIDMOORE, LIONEL D.DIGIACINTO, PETER M.SANCHEZRIVAS, MICHEL
Owner INEOS USA LLC